Apparatus for producing latex foam



March 30, 1954 A. w. KEEN ,6 3,72?

APPARATUS FOR PRODUCING LATEX FOAM Filed June 8. 1950 2 Sheets-Sheet 1 604/ I 0mm 621 m sa r I N V EN TOR. ,azx/w /1 K55 (5W 14.0fm

ATTORNEY March 30, 1954 A. w. KEEN APPARATUS FOR PRODUCING LATEX FOAM 2 Sheets-Sheet 2 Filed June 8, 1950 .51. l 2/ III .1

Illvlllllll fllllltllvlrl'"llllv ATTORNEY Patented Mar. 30, 1954 1. APPARATUS FOR PRODUCING LATEX FOAM Alexis Keen, Wayne Township, "Passaic "County, N. J.; 'assignor;to'United States Rubber Company; New York, N. Y.', a corporation o'f'New Jersey Application June 8, 1950, Serial No. 166,871

-- 9 Claims. (Cl. 26128) This invention relates to apparatus for m'akine foam rubber from natural or synthetic rubber ."latex, so'that the foam rubber or ,sp ge rubber thus produced Will be highly uniform ast'o bubble V duce the. .latex foam.

2 other gas, latex and other materials usedto pro- In order to add ..to "the clearness of thisjdisclosure it is desired to point out that froth. as herein used means soap. or

size and density. 5.. similar froth; foam means latex vfoambefore It is Well known that foam rubber articles may and after it has set or gelled, and sponge means he made. by compounding natural orsynthetic the vulcanized sponge rubber. Furthermore the rubber latex'with certain ingredients, suchas vulterm fmeasure is to be construed broadly as c g ents, accelerat rs, gelling agents and covering, measuring, metering or weighing the "stabilizers; and'then whipping the latex into a 10 materials that are supplied to the foam forming foam; depositing the foam in amold, allowing the apparatus, i'foam to gel by permitting it to restat room tem- An important feature Tof the present invention 'perature 'or'shortening the gelling time by heat, consists of the steps of introducing a soap solua d fi a y'vu c g' h f m ru ber t0 fo m tion and a gas, such as air, into the closed recepthemold'edspo ge rubber article. 15 tank soas to .form a soap froth' that fills the Foam 'rubberiwhen prepared by whipping the receptacle and is forced therefrom under pressure *latex' into a foam has anon-uniform cellular in a uniform stream. A measured amount. of "structure,"since bubbles ofvari0us' sizes are pr0- latex isv then intimately commingled withi'this duced by the air introduced into the latex during stream of soap froth in such a manner thatthe the whipping-operation and the cellistructure is 0 bubbles of the froth are evenly coated with the destroyed to some extent. by themechanical latex.

workingiof the latex afterthe gelling agent has Another important feature of the present inbeen "added. This mechanical working also 'provention resides in shearing means which act upon du ev co u t o in the latex whi h thestream of soap froth .to shear'the same and aus s t e sult e' p e'e ve a t u u 25 thereby reduce the size of the soap bubbles and composed of rubber crumbs held together by fine V produce a froth of uniform cellular structure. fibers. Such a'crumbstructure isweak'and con- The uniform bubble size maybe as large or small 'tains more lllbber'than is yas desired, depending upon. theamount ofshear- These difficulties experienced heretofore; inthe ing to which the froth. is subjected. manufacture of foam rubber. from latex are A further feature of the present inventionconavoided ,by the present inventionfand aifoam' 30. sists in supply ng to the stream .ofsoap froth a "1ub is" produced whioh'is' 'h g 'lynniform in ,metered amou'ntof latex, to which a gelling agent "den'sity'and astothesizepf its-bubbles. This is has been added, so asto cause the. latexto come accomplished by mixing soap froth with'latex in into intimate contact with the froth andform a a'clos'ed' container '50 as'to intimately commingle gelable latex foam, and then delivering thisfoam the'soapfroth'withthe latex?More'particularly, .35 in a few seconds to themold Where it. will set this is accomplished 'by preparing a-soap'froth quickly in the desired shape. that is composed "of bubbleshaving'substantially One important advantage secured byemployy a x W th it in ing the apparatusof the present invention is that such a manner thatthe bubbles ofthes'o'ap'froth by performingithe various operations in a unit are evenly coated-with the latex 'and' the 'BVGILAO that is. entirely enclosed, suflicient pressure may --cellular"structure of the soap 'froth' is mainbe used to eject the latexfoam. fromthe receptained. tacle in a continuous stream,.and to deliver it into Fu'rthenhy employing the present invention a a closed vulcanizing mold. This procedure elimicontinuous streamlin'eddiow of the foamrubber hates the large amount of scrap that usually acissecured;and all'ingredients emp1oyedto'pro-.;45 cumulates as overflow .while the mold is being duceth foam ru'bberare accurately meteredand filled from a mixing vessel. The mold also. fills advanced =-in a -"continuous pressure stream out better when a pressurefeed is used,.as the through the closed foam producing equipment. foam pushes, the air out through the mold vents Thisigiveaaccurate'controlof all materials-that and prevents the formation of low spots or voids f'QImithe foam. $50 which frequently occur in the remote portions of In carrying out the presentinvention. natural the mold. 'Furthermore'the latex foam produced or synthetic =rubber may be :used: and ;various by the present apparatus ishighly uniform and. frothing liquids may be used, e. g., a soap solutherefore flows well into various portions of the tion. The invention makes-possible the accurate -mold. .eccntr 1eefithe amountecfi:.soap-xsolution rair or.-;&5 The apparatus-of-thepresentinventionean be commercially operated without becoming fouled by coagulation of the latex compound on the machine parts. This is due to the fact that all air jets and most moving parts are located in the soap solution and therefore are free from any accumulation of latex. Furthermore the parts over which the latex compound does pass are smooth and streamlined and designed to give the foam a velocity sufficient to cause all surfaces to be scoured continuously with fresh compound and thereby to prevent fouling.

The density and bubble size of the latex foam produced in accordance with the present invention are highly rniform, largely because all the ingredients that form the foam are metered and mixed uniformly and continuously in a closed system. No loss of gases or volatile matters can take place. The variability in cell size of foam made in an open beater, which is a common source of trouble, is thereby avoided in the present invention.

The froth structure is under control at all times. The original soap froth is controlled as to bubble size, by the size of the hollow needles used to inject air into the soap solution. Furthermore reduction of the bubbles of the soap froth to the desired fineness is controlled by the amount of shearing to which they are subjected in the shearer.

The mechanical operations employed in mix-- ing the latex, to which a gelling agent has been added, with the soap froth are redrced to a minimum by the present procedure. This is highly desirable since excessive mechanical working of the latex after the gelling agent has been added produces a latex coagulum having a crumb struc-- ture tied together with fine fibers of low strength.

Furthermore the apparatus is so designed that the latex is rapidly intermixed with the soap froth, and remains in the apparatus only a short time. This rapid intermixing and removal of the latex is especially advantageous as it further insures against coagulation in the apparatus.

The pressure in the apparatus is preferably maintained above atmospheric, with the greatest pressure in the frothing chamber, and a gradually diminishing pressure in the successive stages of the process until, at the exit of the apparatus the pressure is equal to atmospheric.

The above atmo pheric pressure is obtained in the apparatus by creating a resistance to flow in the various stages of the process while keeping the pressure at which the air enters the frothing chamber constant. For example, the pressure in the frothing chamber will be equal to the back pressure resulting from the restricted passage of th froth through the shearer. The pressure in the apparatus may of course be varied by adjusting the clearances in the froth and latex foam passage. By maintaining the pressure in the apparatus above atmospheric the froth and foam are forced therethrough in a smooth and continuous manner. Furthermore it is possible to produce very low density foam due to the expansion of the froth and foam as the pressure decreases. By forming th froth under pressure, its speed of passage out of the frother into the shearer is substantially slower. This enables the froth to dra n before it leaves the frother and accordingly reduces the dilution of the latex when the froth is mixed with it. Finally by processing the soap '"roth and foam while their volume is smaller than it would be at atmospheric pres r, the tenency for breakdown of the cellular structure is substantially reduced.

The present invention is important in the manufacture of molded latex foam mattresses, pillows and seat cushions, because it makes possible the production of such articles with the desired cushioning action, but with less latex therein than is in the latex foam cushions made by the prior practice. The saving in latex is due to the formation of a latex sponge having a high-- ly uniform cell structure and accordingl the absence of the latex crumb structure and fiber which is frequently present in the latex foam articles made by the prior methods. Furthermore, when molded articles are constructed of latex foam prepared in accordance with the present invention, the increased strength of the foam makes possible the removal of the hot, freshly molded articles from the mold with much less damage due to tearing than heretofore.

The present invention is also important in manufacturing latex foam flat stock or sheet material of various thicknesses, which is used to make upholstery stock pads, powder puffs and various articles used for cosmetic purposes. This is because the highly uniform cell structure of the foam gives it added strength. Furthermore when the sheet stock is split into thinner sheets, as is frequently done, uniform cell structure increases the value of the split sheets.

Today there is a large demand for highly uniform latex foam. By avoiding an uneven cellular structure and the formation of objectionable crumb or fiber in the latex, it may be readily seen that the present invention enables the preparation of this more desirable type product.

The principal apparatus used in carrying out the present invention comprises: (1) a closed. frother in which jets of air are forced through a soap solution to form the soap froth, (2) a shearer in which the size of the bubbles of the soap frothis reduced by a shearing action, and (3) a mixer in which the light weight soap froth and relatively heavy latex are brought together and intimately commingled to form latex foam.

The above and other features of the present invention will be further understood from the following description when read in connection with the accompanying drawings which illustrate good practical constructions for carrying out the present invention.

In the drawings,

Fig. l is a vertical sectional view of apparatus constructed in accordance with the present invention;

Fig. 2 on a larger scale is a vertical sectional view through the froth shearing mechanism and latex distributing cup shown in Fig. 1;

Fig. 3 is a perspective view of a small piece of sponge rubber having the highly uniform cells secured by the present invention; and

Fig. 4 is a sectional perspective view of a modifled construction for thoroughly intermixing the latex and soap froth.

Referring first to Fig. 1 of the drawing in which the parts are shown more or less schematically, the principal portion of the apparatus is supported by the upright posts In which rest upon the floor or other supporting surface ll. These uprights are connected by the transverse braces IZ. This structure serves to support a closed receptacle l3 having a cylindrical body which is closed at the lower end by a floor I4, and at the upper end by the rounded dome I5.

Closed frother This receptacle l3 forms a closed frother and dama es :hasprovided the: seeondnfloor zl Erin; spaced relaion td:the.:floor l4;;;-so:as;to.form an airchamber betweenuithese; floors. Thor-floor .l 6-.is provided rwith alarge: numberi'of hollow needles 1H that preferablyproject. upwardly. a: short distance fifromrthei fioor. :as shown;;and are spaced about EinCh' :apart. Thetoutside. diameter of these pneedles isimportant :as it controls, thesize of -;-the+bubb1es. This outside diameter. may vary 'fromwabout: -.007".;to- .02". -The inside bore of ithe needless. iswless' important and need not be moredshan-about .008".- in diameter. The acv-tion of theseneedlesissuch that when a frothing iwliquid, such as a soap-solution, isdeposited upon athenfloor .16 to a. height-.-.above the level :of the top of theineedlesrbyvmeans to be described, air or other gas; which isforced intor the" space 1 between the-floorsl4 and::l6, willpass upwardly i through the :needles .l! and :through. "the soap solutionupon the floor I 6. .Ihisproduces a M5084) froth lax-that is 'highlyuniform as to bubble -size--in sufficient quantity to: fill the interior of --.--the receptacle-13. Thissoap frothescapes from the-receptacle 13,, inithe construction shown, through. acentral downwardly extending pipe -..-or passagerlfl that: passes through. the floors: l4 and 16. The upperiend .of this pipe terminates aishortdistance-below;the dome l5. While the .size of the bubbles. formed-in thereceptacle l3 twill-depend upon-the size of the needles ll, it will dependalso on. thepressure'in this receptacle. Ehe vdensity-ofthe froth'should be less than .01 ;-.and preferablybelow .005 gram per cubiccentimeter.

-An important feature of the present invention, as above pointed out,--resides in the closed receptacle l Bandmeans for supplying a-metered quan- ..tity of:the materials used-to form the soap froth to-the interior'ofthis receptacle. In the con- .structionshowm a' soap solutionqconta ned in a tank I9 issupplied to the-receptacle is through the :pipes 20 and *2l,.-thc-latter-of which delivers the soap solution into the receptacle above the floor .16. Inorder to supply a metered or-measured quantity of-thissoap solution tothe recep- -tacle..-I3, a metering pump -22 of wellknown construction, and preferably a gear metering pump, 1. is employed. At. the same time,- air or other gas such as nitrogen :in a. metered stream is supplied to. the-chamber between thefloors 14 and-l6 by.

thepipe23leading fromthe intake head -24 to a meteringprmp 25 and by. the-pipe 26 -leading from this pump .to the chamber below the-hollow ..:needles I1. ,As aresult-of-this'construction, the ...air;s.upplied.,by the. needles 1! passesupwardlv .through the soap solution to form asoap froth F.

- .This soap-froth is preferably subjected. inthe receptacle] 3, to a greater thanatmosphericprea sure, for. .example an added pressureof from 5 to 10 pounds. .This. will cause the froth F 'to pass downwardly. within the pipe I8, in. a continuous stream as indicated by arrows. ..As thefroth rises in ,thereceptacle 13 the excess soap solution can drain therefrom to .the floor. I 6.

Shearer 2..of.the. drawingssis mountedin apasing. 21::at-

i.-.-.,taohed..to.the 1ower...fioor A 4, Thet-loivemend of 1.:the pipe'l8 leads to this casing. "Within the casing 2'! are provided a number of concentric cirxcular bands comprising rotating bands 28-, and

bands positioned so that. the rotating-bands rotate between the fixed bands. The fixed bands comprise an upper set 3| which extend down- :wardly from the floor It and a lower set 29 which extend upwardly from a floor 3B of the container ,21. The rotating bands 28 are secured to a rotor or disc-32 so that some of these bands extend upwardly from the rotor and others extend down- 'wardly from'the rotor as will be apparent from "'Fig; 2. -and rotating bands is preferably about ,4 All ofthe bands .28, 29 and 3| are provided with the The clearance space between the fixed ,apertures 33 through which the soap froth may .pass as indicated by the arrows in Fig. 2. Some .of the soap froth may pass around the edges of .thefixed and'rotating bands, but most of .the

froth passes through the holes 33. The froth enters the shearer from the pipe l8 and passes o-twardly around the outer edge of the rotor 32 and then inwardly below the rotor as shown.

' The rotor 32 in the construction shown is rigidly secured to thelower end of a hollow shaft 34. which extends upwardly through the'pipe l8 and through a bearing in the top of the dome l5 .anism within the casing 38. The size of the bubv bles forming the soap froth can be reduced as desired by controlling the speed of the rotor 32.

If. a coarse froth is desired, this rotor should be turned slowly and if a fine froth is desired, the

rotor should be rotated more rapidly. For a soap froth having adensityof about .0? 5 a linear speed notin excesscf 300 feet per minute may be employed without injuring the foam structure.

-While ashearing mechanism such as just described is usually desirable, it is not necessary ...in allcases, for if a coarse cell structure is desired the shearing step may be omitted. In place of the shearing mechanism herein shown, the

soap froth may be formed and sheared in the same receptacle by using a construction substann tially thesame asthat shown in my Patent No.

. 2,335,339, provided the soap solution is supplied tothe hollowneedles or air jets, and the recep- .tacle is closed so that an above atmospheric pressuremay be built up therein.

.-It is essential in carrying out the present invention that the soap froth, whether coarse or fine, have intimately mixedtherewith a rubber -latex compound so as to form the desired latex -foam. .-Argood practical form of apparatus for intimately intermixing the liquid latex with they soap, froth will now be described.

Miner Thedensity of; thesoap froth will decrease as Z,itprogresses through the apparatus becausethe 1 back. pressure decreases and permitsthe soap bubbles to expand. The density of the soap froth .up-on reaching the mixing area may beyfor example, about .695 grain per cubic inch. The density'ofethe 'liquid latex as it enters the mixing areais about 1.0. This very great diiference in $113 density of the two materials makes it difficult to mix them'thoroughiy without crushing -.the soap froth. "One highly desirable constructronafortintimately: mixing the latex compound wrwith. aidiewingxstream 1 of soap frothis -shown-in Figs. 1 and 2 of the drawing and will now be described. A supply of natural or synthetic latex containing the usual sulphur and other compounding materials is confined within a container 39 which is connected by a pipe 40 to a metering pump 4! which pump has leading therefrom the pipe 42 adapted to supply the latex to the stream of soap froth. The casing 21 in which the shearing mechanism is housed has extendingdownwardly from the lower wall thereof a pipe 43, and within this pipe the latex distributing cup 44 is supported in a manner which enables it to rotate. This cup has the outwardly flaring sidewalls shown, and it is concentrically secured to a driving shaft 45 which extends upwardly through the hollow shaft 34 and is supported from the upper end portion of the machine by a bearing 46 mounted on a support 47 and a gear 48 which is driven by a pinion 45. The pinion 49 is driven at the desired speed by a variable speed mechanism mounted in the casing 50.

The feed pipe 52 extends inwardly through a hole in the side wall of the pipe 43 and into position to deliver its stream of latex into the cup 44 as best shown in Fig. 2. It is important to add a gelling agent to the latex at about the time it contacts the soap froth. This is done in the construction shown by providing a tank 5! containing a gelling agent. This tank is connected by a pipe 52 to a metering pump 53 which 0 pump has leading therefrom a pipe 54 that communicates with the latex feed pipe 42 so as to inject a metered amount of the gelling agent into the latex stream with a turbulent action thereby causing the gelling agent to be mixed thoroughly with the latex before the latex enters the cup 44.

Instead of supplying the gelling agent to the latex stream in the manner just described, the pipe 54 may discharge directly into the cup 44. It is also possible to add the gelling agent to the soap solution so as to introduce it into the latex with the soap froth. The density of the latex foam is determined by the density of the soap froth and by the proportion of latex and soap froth mixed together.

The size of the cup 44 relative to the bore of the pipe 43 is important since the cup serves to reduce the size of the passage through which the soap froth is forced and wherein the soap froth is intimately commingled with the latex. During mixing, the latex is thrown outwardly, by the centrifugal force of the rotating cup, over the upper edge of the cup to contact the stream of froth moving downwardly along the inner walls of the pipe as shown in Fig. 2. The size of the annular passage provided between the outer periphery of the cup 44 and inner wall of the pipe 43 may vary from about e sof an inch in width to A; of an inch, depending upon the strength and size of the bubbles forming the froth passing through this annular passage. The preferred size or". this passage is between and /8 of an inch.

The mixing cup 44 should be so designed that during operation it will always contain a fresh supply of latex and never hold a portion of latex long enough for it to coagulate therein. The continued flow of latex from the rotating cup may be best insured by using a shallow cup having tapered walls as illustrated in Figures 1 and 2. In actual practice using a cup having a l /z inch outer diameter, it was possible to produce two cubic feet of latex foam per minute.

It is important that the latex be mixed uniformly through the soap froth stream in order that a uniform latex foam will be produced. The

mixing technique just described helps to secure this uniform mixture but the cu should not be rotated at a speed that will cause the froth to break down. Usually 600 linear feet per minute is about the highest speed at which the outer edge of the cup should rotate, as at higher speeds the mixing action becomes too turbulent and causes the soap froth to break down. The mixing of the materials is further secured, in accordance with the present invention, by mounting on the lower portion of the revolving shaft 45 the feed screw 55 which extends downwardly a substantial distance within the pipe 43 as shown. This feed screw helps to mix the latex with the froth so that the latex will cover the soap bubbles and form the desired latex foam.

The feed screw serves also to help feed this foam downwardly within the pipe 43 through a restricted opening at its lower end and into a mold such as shown in Fig. 1. This mold, which consists of the lower molding section 56 and upper molding section 51, is of usual construction and may have the inwardly projecting cores 58. The latex foam is fed to this mold through a flexible pipe 59, one end of which is secured to a connector 60 attached to the lower end of the pipe 43. The other end of the pipe 59 has secured thereto a nozzle 6| adapted to be inserted in a hole in the upper mold section 51 so that the latex foam may be forced under pressure into all portions of the mold to completely fill the mold. The air vents 58' are provided in the mold sections so that the air may escape from the mold cavity while it is being filled with foam.

It is desired to point out that the construction and arrangement of receptacle [3 and pipe 43 are such that the latex is delivered into the stream of soap froth so that it will not enter the receptacle l3. Attention is called to this because if latex is permitted to enter the receptacle I3 or the shearer in the receptacle 2'! it would become deposited on the apparatus therein and interfere with the proper operation of such apparatus.

When the apparatus of the present invention is employed, the gelling agent used preferably is of suflicient concentration to operate very rapidly and cause the latex foam to set or gel quickly after it enters the mold, since the quicker the foam sets the less change there will be in the latex bubbles forming the foam. By employing the construction shown in the drawing, only a few seconds need elapse from the time the gelling agent is mixed with the latex until the latex foam is formed and forced into the mold cavity.

By employing the driving means shown in the drawings, in which one shaft is provided to rotate the cup 44 and feed screw 55, and another and independent shaft 34 is employed to rotate the shearer, the speed of one may be varied without changing the speed of the other. It is usually desirable to rotate the cup and feed screw faster than the shearer.

The four metering pumps 22, 25, 4| and 53 are all shown as driven from a power shaft 62 which is rotated at the desired speed by a variable speed mechanism within the housing 63. Each pump may be driven at the desired speed by employing the proper ratio between the driving gear 64 and driven gear 65. This makes possible the supplying, as a continuous stream, of any desired metered quantity of soap solution, air, latex and gelling agent to produce a soap froth of the proper density, and a latex foam of the desired density and cell size. By mixing these materials in a closed air-tight receptacle an ':accurate" control can "be maintained or theliquids and gases that aifectxthe --finalproducts Furthermore, *by' building up .a pressure within the receptacle l3 to'secure a force'feedfia rapid movementof the stream of soap froth out-. of this -5 receptacle-is secured and the'la'tex-fo'am: is quickly formed and forced intothe mold to-produce sthe desired sponge article. 1

After themold 5t, 51' has been 'filledit mayhem moved into a :vulcanizer' to vulcanizeithe 'latex m foam. as :heretofore, and thereby produce a ished latex sponge pillow or-otherz-article hav ing theuniform cell structure shown inFi'gt 3 wherezthe small circles-C lindicate thexscellu structure.

The.pressure maintained-in the closed receptacle i3 is determined largely by the back pres-s sure built upas the soap froth' F :passes through the shearer, and .is then mixed with the' latex and. is finally. discharged through the; flexiblev pipe; 59.2. This back pressure. not. only :causes the froth Fto flow .through thezapparatusrina unifornmstreamxbut servesaalso. to influence the density of the soap froth, and accordingly theq; density ofthe finalzspongesproduct. 1

In. some cases. the revolving cupill l. alonemay: give sufficient mixing, butcusually an:additional;.. mixing action is .desired; such aspro'du'ced by. the... feed screw 55'shown in Figs. 1 and 2, 0r;by.the'dife; f erent form: of mixer shownxin Fig: 4. Inigthi's modified constructiorra power shaft such as451has. secured thereto belowthe .cup. 44" a .numberaof spaced disksfifiii. There: are; also. provided be-. tween. the, disks 166-:the oppositely :extending. blades or paddlesqfi'l thatztend. totscrapethelatex foam from. the; inner; walls ;.0f;..the: tube .43... At: the lower. end of.the.shaftz45iszprovided a spider; 1 68 that is rigidly mounted in the tube 43 and looselyliembraces theshaft 45. To the lower end of the tube 43 is secured the connector 69. The arrangement. is such that. the latex foam is re.- peatedly squeezed to a thin stream as it moves downwardly past' one disk-'66 after another. This brings the latex into intimate contact with 5. the soap. froth without crushing the froth.

'I'he'apparatus herein described may be oper-1 ated at room temperature. a

One suitable latex compound that'may be used in carrying. out the presentsinvention is the. following, the parts being b weight...

v Naturallatex (ammonia preserved, 68% solids)---" Foam stabilizerdtrimene base): 1 Composite curative paste (60% solids) Sulfur Accelerator Zinc oxide xna fffiit i itraisins:::::::::::::: 1

(Adjust total. solids to 58% The usual vulcanizing ingredients and antioxidants are used in the latex. The stabilizer (trimene base) is added to the latex to give better control of the setting or gelling time but is not essential.

A gelling agent is essential and any of the well known latex gelling agents may be used. Suitable gelling agents are sodium or potassium silicofluoride. These may be added to the latex through the pipe 54 of the drawing, or they may be mixed with the frothing solution and thereby mixed with the soap froth and latex.

Any of the common good frothing soaps may be used in this apparatus, such as, potassium oleate, sodium oleate, the stearates etc. A .5% to 3% concentrated aqueous solution of the soap is most satisfactory. Gases other than air may be used to form the soap froth provided they are comparatively unreactive with the latex.

It 'will "be seen from the foregoing that the s hollow needles if produce'soapbubblesthat are highly uniform asto size; and: that the shearerl serves to reduce the diameter-of thebubbles to produce uniformbubbles of smaller size. It will.

also be urrderstood that the density of the soap... froth is controlled largely by the I back; pressure- A in the -apparatus. This. pressure will diminish: graduallythrough the apparatusso .that/the 'bubbles-x will expand a substantial amount whilec passing through the several stages ofthe proce-z ess-.-- Such expansion may reduce the densityof the bubbles as much as one-half. This low den-J. sity-froth makespossiblethe formation of a low 1 density latex foam. This low density and .uni' fornn'latex foam makes possible'ia substantial savingin the' 'amount of latex required'to :produce' a cushion or-other latex rubber article of a deal sired resiliency."

Having thus described my invention, what l I claimand desire to protect by Letters'Patent is 1. Apparatus for producing a latex foam in a continuous stream; comprising a receptacle, a :a restricted discharge passageleading from the up- .1

"per portion of said receptacle, said receptacle and.

said dischargepassage being completely closed-J to the-atmophere except at the. latex foamexit endof said discharge-passage to'providea closedsystem in which a pressure above atmosphericm. can be maintained whereby'froth can flow underk a continuous pressure gradient through itsxpath": to the exit end of the discharge passage for-the. latex foam, means forintroducing a soap solu-l tion into thelower. portion-of Jsaid .receptacle,i=. means for introducing into'saidsoap-solutionw air at- -a pressure sufficient to maintain-an above atmospheric pressure said receptacle, means: for delivering a metered quantity of latex into I said discharge passage 'ata point below: the -re-: cepta'cle, and a mixer within said dischargepassage between the point at which the latex is troduced and the exit'end of said discharge passage for inter-mixing said latex with .the I soap f-rothpassing through said 1 discharge passage.

2. Apparatus for producing a highly uniform latex-foam in a continuous stream; comprising a closed receptacle having a restricted discharge passage leading from: the upper" portion ofsaid receptacle, said receptacle and said "discharge passage being completely closed to the iatmos phere' except at the latex foam exit end: of 'saida discharge passage to p-rovide a closed systemnirrs whichna pressure.aboveatmospheric-can be main-. a tained whereby; froth can now underacontina uous pressure gradient through :itsentire 'pathit to the exit end of the. discharge passage forzthen latexioamy: means. for supplying. a lfrothing iiqfe: I uid to the lower portion of said receptacle, means for supplying jets of gas to the receptacle at a pressure sufficient to maintain an above atmospheric pressure in said receptacle and to pass through the liquid so as to form a froth that fills the receptacle and flows out uniformly under pressure through said passage, means for introducing a metered quantity of latex into the formed froth, and a rotating distributor in said discharge passage before the latex foam exit end thereof operable to distribute the latex through the froth stream after it leaves the receptacle and to bring the latex into intimate contact with the froth bubbles to form. a latex foam.

3. Apparatus for producing a highly uniform latex foam in a continuous stream, comprising a receptacle, a discharge pipe leading from the upper portion of said receptacle, means for supplying soap solution to the receptacle at a regulated rate, said receptacle being completely closed to the atmosphere except through said discharge pipe, means for supplying jets of pressurized air to the receptacle at a regulated rate to maintain a pressure above atmospheric in said receptacle and to pass through the soap solution so as to form a soap froth that fills the receptacle and flows out uniformly through said pipe, means for continuously introducing latex in a metered stream into the formed froth, and a rotating distributor down stream of said receptacle and in said froth stream operable to distribute the latex through the froth stream and bring the latex into intimate contact with the froth bubbles to form a latex foam.

4. Apparatus for producing a highly uniform latex foam in a continuous stream, comprising a receptacle having a discharge passage leading from said receptacle, said receptacle and said discharge passage being completely closed to the atmosphere except at the latex foam exit end of said discharge passage to provide a closed system in which a pressure above atmospheric can be maintained whereby froth can flow under a continuous pressure gradient throughout its entire path to the exit end of the discharge passage for the latex foam, means for supplyin a frothing liquid to the lower portion of said receptacle, means for supplying jets of pressurized gas to the receptacle to maintain an above atmospheric pressure therein and to pass through the frothing liquid so as to form a froth that fills the receptacle and flows out uniformly under pressure through said passage, a rotating cup supported in the froth stream in said discharge passage before the latex foam exit end thereof operable to distribute the latex through the froth stream after it leaves said receptacle, said cup having a narrow clearance with the walls of the discharge passage, means for introducing a metered quantity of latex into said cup, and means for rotating said cup so that the latex therein will be thrown outwardly by centrifugal force and flow over the edge of the cup and into the froth stream to form latex foam.

5. Apparatus for producing a highly uniform latex foam in a continuous stream, comprising a closed receptacle having a restricted discharge passage leading from the upper portion of said receptacle, said receptacle and said discharge passage being completely closed to the atmosphere except at the latex foam exit end of said discharge passage to provide a closed system in which a pressure above atmospheric can be maintained whereby froth can flow under a continuous pressure gradient through its entire path to the exit end of the discharge passage for the latex foam,

means for supplying a frothing liquid to the lower portion of said receptacle, means for supplying jets of gas to the receptacle at a pressure sufficient to maintain an above atmospheric pressure in said receptacle and to pass through the liquid so as to form a froth that fills the receptacle and flows out uniformly under pressure through said passage, shearing means for the froth stream operable to reduce the size of the froth bubbles, means down stream of said shearing means for introducing a metered quantity of latex into the formed froth, and a distributor in said discharge passage before the latex foam exit end thereof operable to distribute the latex through the froth stream and bring the latex into intimate contact with the sheared froth bubbles to form a latex foam.

6. Apparatus in accordance with claim 5 in which the distributor comprises a rotating member having a narrow clearance with the walls of said discharge passage whereby the latex and froth are intermixed in a narrow zone between said distributor and the walls of said discharge passage.

7. Apparatus in accordance with claim 6 wherein the shearing means comprises a rotating member in said discharge passage, and means for independently rotating said shearing means and the distributor.

8. Apparatus in accordance with claim 5 including means for delivering a metered quantity of gelling agent into the froth stream.

9. Apparatus in accordance with claim 5 including a feed screw down stream of said distributor and before the latex foam exit end of said discharge passage operable to deliver the latex foam under pressure to the exit end.

ALEXIS W. KEEN.

References Cited in the file of this patent UNITED STATES PATENTS Number Name Date 1,582,992 Loepsinger May 4, 1926 1,885,785 Thompson Nov. 1, 1932 2,114,275 Murphy et al Apr. 12, 1938 2,261,439 Kelly Nov. 4, 1941 2 290,729 Blair et al July 21, 1942 2,290,736 Buffington July 21, 1942 2,295,740 Keen Sept. 15, 1942 2,307,082 Te Grotenhuis Jan. 5, 1943 2,335,339 Keen Nov. 30, 1943 2,381,380 Carter Aug. 7, 1945 2,441,235 Bfair et a1 May 11, 1948 2,572,049 Oakes Oct. 23, 1951 2,581 918 Spencer Jan. 8, 1952 

